CN1446752A

CN1446752A - Method for preparing polymeric ferric sulfate by using partial oxidation process

Info

Publication number: CN1446752A
Application number: CN 02147656
Authority: CN
Inventors: 郑雅杰; 龚竹青; 刘兴渝; 占寿祥; 陈白珍
Original assignee: YUNFU SULFUR-IRON ORE ENTERPRISE GROUP CORP; Central South University
Current assignee: Yunfu Guangye Pyrite Group Limited; Central South University
Priority date: 2002-10-22
Filing date: 2002-10-22
Publication date: 2003-10-08
Anticipated expiration: 2022-10-22
Also published as: CN1233561C

Abstract

A process for preparing polymerized FeSO4 (PFS) by partial oxidization method includes dissolving the 3-valence Fe contained ore or slag in sulfuric acid, adding FeSO4, partial oxidizing with strong oxidizing agent (chlorinate, H2O2, or nitric acid) to obtain liquid PFS, concentrating, and drying to obtain solid PFS, which can be used to treat life sewage or the sewage containing heavy metal.

Description

Partial oxidation process prepares the method for bodied ferric sulfate

The present invention is to contain the technology that the ferric iron waste residue is feedstock production bodied ferric sulfate (PFS).

As the poly-iron of inorganic water purification agent, because preparation bodied ferric sulfate PFS is that the employing green vitriol is a raw material, with Fe ²⁺Be converted into Fe ³⁺, and Fe ³⁺Derive from ferrously fully, adopt the amount of the oxygenant that oxymuriate or hydrogen peroxide oxidation consumed big, thereby increased production cost; Though utilize to contain ferric ore or waste residue prepares the consumption that bodied ferric sulfate PFS can reduce oxygenant, exist of poor quality, the unmanageable problem of bodied ferric sulfate PFS basicity in the production.

The objective of the invention is to overcome above-mentioned shortcoming, and provide that a kind of speed of response is fast, good product quality, pollution-free, the method for preparing bodied ferric sulfate that cost is low.

Technical scheme of the present invention is:

The sulfuric acid that at first will contain ferric pyrite cinder or ore, slag and 30～60% reacted 0.5～5 hour being lower than under 130 ℃ of conditions, and its reacting liquid filtering obtains pickling liquor;

Then, in pickling liquor, add iron sheet or iron filings, under being lower than 110 ℃ condition, react Fe to the solution ³⁺After reducing fully, after filtration, crystallisation by cooling obtains green vitriol;

Then in pickling liquor, add green vitriol (FeSO ₄7H ₂O), under ℃ condition of temperature of reaction 〉=40, add sodium chlorate or Potcrate or hydrogen peroxide or nitric acid simultaneously, treat Fe in the solution ²⁺Complete oxidation obtains combining red liquid PFS;

Again with liquid PFS evaporation, concentrate, under 60 ℃～120 ℃ conditions, after stirring dry or concentrating the back room temperature and deposit efflorescence, dry down in 60 ℃～120 ℃; Dried solid PFS is pulverized, obtain the Powdered PFS of faint yellow solid, its crystalline structure is Fe _4.67(SO ₄) ₆(OH) ₂20H ₂O.

Advantage of the present invention is:

(1) utilization contains the ferric iron waste residue and prepares PFS, has reduced the oxygenant consumption, has reduced production cost;

(2) utilize FeSO ₄Adjust the PFS basicity, guaranteed quality product;

(3) obtained liquid PFS iron level is up to more than 14%, and easily evaporation concentration, drying obtain solid PFS;

(4) bodied ferric sulfate of producing with the present invention (PFS) is used to handle sanitary wastewater and heavy metal wastewater thereby is effective.

Be described further below in conjunction with accompanying drawing and embodiment:

Fig. 1 prepares the pickling liquor process flow sheet;

Fig. 2 prepares the green vitriol process flow sheet;

Fig. 3 prepares liquid PFS process flow sheet.

Fig. 1 has described the processing step of preparing polymeric ferric sulfate by using partial oxidation process of the present invention.

1. the preparation of pickle liquor

The sulfuric acid that will contain ferric pyrite cinder or ore, steel-making waste residue and 30～60% reacted 0.5～5 hour being lower than under 130 ℃ of conditions, then reacting liquid filtering was obtained pickle liquor; Its specific embodiment is seen accompanying drawing 1.

2. the preparation of green vitriol

Get above-mentioned pickle liquor, add scrap iron skin or waste iron filing Fe in the reaction solution under being lower than 110 ℃ condition³⁺After reducing fully, after filtration, crystallisation by cooling obtains green vitriol; Its specific embodiment is seen accompanying drawing 2.

3. the preparation of liquid PFS

According to remaining H in the above-mentioned pickle liquor⁺Concentration and product basicity add a certain amount of green vitriol (FeSO in pickle liquor₄·7H ₂O), under ℃ condition of reaction temperature 〉=40, add simultaneously an amount of sodium chlorate or potassium chlorate or hydrogen peroxide or nitric acid, treat Fe in the solution²⁺Complete oxidation obtains combining red liquid PFS, and its partial oxidation process prepares liquid PFS specific embodiment and sees accompanying drawing 3.

4. the preparation of solid PFS

Liquid PFS is evaporated, concentrates, under 60 ℃～120 ℃ conditions, dry under 60 ℃～120 ℃ after stirring drying or concentrating rear room temperature Store erushing. Solid PFS after the drying is pulverized, obtain the Powdered PFS of faint yellow solid, its crystal structure is Fe_4.67(SO ₄) ₆(OH) ₂·20H ₂O。

Embodiment:

Embodiment 1:

1. the preparation of pickling liquor, (the Guangdong cinder of pyrite ore from Yunfu Pyrite Mine, it burns slag and contains Fe to get pyrite cinder 3000g after the oven dry ₂O ₃74.1%, Fe ₃O ₄15.96%, FeO0.5%), add 50% sulfuric acid 7740ml at three and the neck bottle of 10L; Start to stir, littlely add above-mentioned pyrite cinder slowly, when reaction soln during near boiling, stop to feed in raw material, begin again when temperature of reaction is lower than 110 ℃ to feed in raw material, temperature of reaction is maintained 110～120 ℃, total reaction time is controlled to be 4 hours; Reaction back thin up is 3mol/L to total concentration of iron, and filtered while hot gained filtrate is pickling liquor, keeps filtrate for the second time.

2. the preparation of green vitriol, with for the second time filtrate and water the molten dilution of part acidleach being caused total concentration of iron is 1.8mol/L, constantly stirs down, adds capacity iron filings or iron sheet, is warming up to 70 ℃, treats Fe in the solution ³⁺After reducing fully, filtered while hot, crystallisation by cooling, filtration, centrifuge dehydration promptly obtain green vitriol in 60 ℃ of oven dry.

3. acid dip solution 1L is got in the preparation of liquid PFS, and the green vitriol or the industrial by-products green vitriol 1070g of method for preparing added in this pickling liquor, be heated to 60 ℃ after slow plain silk fabrics add sodium chlorate, treat Fe in the solution ²⁺By complete oxidation, obtain combining red liquid PFS.

4. the preparation of solid PFS continues heating, vacuum concentrated liquid PFS and is higher than 16% to total iron content, then under 60 ℃ condition, stirs dry faint yellow solid PFS, and pulverizing afterwards is pale yellow powder PFS, and its basicity is 10%.

Its quality product is as shown in table 1: solid PFS quality is better than national standard.

Table 1 solid PFS sample quality and national standard are relatively

Index	Full iron/%	???Fe ²⁺/％	Basicity/%	The pH (/ % aqueous solution)	??As/％	??Pb/％	Insolubles/%
Index	Full iron/%	???Fe ²⁺/％	Basicity/%	The pH (/ % aqueous solution)	??As/％	??Pb/％	Insolubles/%	Solid PFS	????19.11	???0.02	???10	????2.37	??0.0007	??0.0015	????0.036
GB14591-93	????18.5	???0.15	???9.0～14.0	????2.0～3.0	??0.0008	??0.0015	????0.5	Solid PFS	????19.11	???0.02	???10	????2.37	??0.0007	??0.0015	????0.036

With the liquid of above-mentioned gained and solid PFS flocculation treatment pH=7.13, CODcr=143.9mg/L, turbidity SS=53mg/L is sanitary sewage.Fe in sewage ³⁺During for 28mg/L, remaining CODcr is 47.7mg/L behind the solid PFS processing sanitary sewage, and the COD clearance is 67.4%, and remaining turbidity is 2.4mg/L, and turbidity removal rate is 96.0%.Sanitary sewage is after liquid PFS handles, and the CODcr clearance reaches 62.7%, and turbidity removal rate reaches 93.9%.

Embodiment 2:

Add 50% sulfuric acid 7042mL in the three-necked bottle of 10000mL, start and stir, slowly add the pyrite cinder after the above-mentioned oven dry of 3000g, keeping temperature of reaction is 115 ℃, reacts 4 hours after-filtration and gets pickling liquor;

Get pickling liquor 1L, add the green vitriol 1070g that method for preparing obtains; Then slowly add sodium chlorate behind the heat temperature raising to 60 ℃, treat Fe ²⁺Caused iron level by evaporation concentration behind the complete oxidation and reach after 16%, again after cooling, ageing, gelation, efflorescence in 60～80 ℃ of dryings, pulverizing, obtain faint yellow PFS powder, its basicity is 12.49%.

PFS with method for preparing handles manual simulation's heavy metal containing sewage, Cu in its heavy metal containing sewage ²⁺, Pb ²⁺Concentration is 10mg/L.Get this heavy metal containing sewage 500mL, regulating the pH value with 2mol/LnaOH solution is 10.25, adds PFS and causes Fe ³⁺When concentration is 2.76mg/L, Cu after the flocculation treatment ²⁺, Pb ²⁺Clearance reach 84.4% and 93.1% respectively.Control heavy metal containing sewage endpoint pH is about 6.8, adds PFS and causes Fe ³⁺When concentration is 13.8mg/L, Cu ²⁺, pH ²⁺Clearance reaches 88.7% and 99.2% respectively.

Claims

1. partial oxidation process prepares the method for bodied ferric sulfate, it is characterized in that:

Then, in pickling liquor, add iron sheet or iron filings, Fe in the reaction soln under being lower than 110 ℃ condition ³⁺After reducing fully, after filtration, crystallisation by cooling obtains green vitriol;

2. partial oxidation process according to claim 1 prepares the method for bodied ferric sulfate, it is characterized in that:

1. the pyrite cinder 3000g after the oven dry is got in the preparation of pickling liquor, adds 50% sulfuric acid 7740mL at three and the neck bottle of 10L; Start to stir, littlely add above-mentioned pyrite cinder slowly, when reaction soln during near boiling, stop to feed in raw material, begin again when temperature of reaction is lower than 110 ℃ to feed in raw material, temperature of reaction is maintained 110～120 ℃, total reaction time is controlled to be 4 hours; Reaction back thin up is 3mol/L to total concentration of iron, and filtered while hot gained filtrate is pickling liquor, keeps filtrate for the second time.

4. the preparation of solid PFS continues heating, vacuum concentrated liquid PFS and is higher than 16% to total iron content, and under 60 ℃ condition, stirring drying or ageing get faint yellow solid PFS to efflorescence then, and pulverizing the back is pale yellow powder PFS, and its basicity is 10%.

3. partial oxidation process according to claim 1 prepares the method for bodied ferric sulfate, it is characterized in that:

Get pickling liquor 1L, add the green vitriol 1070g that method for preparing obtains; Then slowly add sodium chlorate behind the heat temperature raising to 60 ℃, treat Fe ²⁺Caused iron level by evaporation concentration behind the complete oxidation and reach after 16%, again after cooling, ageing, gelation, efflorescence in 60～120 ℃ of dryings, pulverizing, obtain faint yellow PFS powder, its basicity is 12.49%.